JPWO2017169682A1 - Metal-containing cluster catalyst, carbon dioxide reduction electrode and carbon dioxide reduction apparatus using the same - Google Patents

Abstract

An object of the present invention is to provide a metal-containing cluster catalyst capable of promoting / controlling the reduction reaction of carbon dioxide with high catalytic activity and selectivity, as well as an electrode for carbon dioxide reduction and a carbon dioxide reduction device using the same. A metal-containing cluster catalyst is a catalyst used to reduce carbon dioxide, the catalyst comprising gold, silver, copper, platinum, rhodium, palladium, nickel, cobalt, iron, manganese, chromium, iridium and ruthenium. It is a cluster comprising one selected metal atom (M).

Description

  The present invention relates to a metal-containing cluster catalyst, an electrode for carbon dioxide reduction and a carbon dioxide reduction device using the same.

  In general, a catalyst is a substance that changes the reaction rate of a substance system that causes a chemical reaction and does not change itself. Depending on the type of catalyst (material, form, etc.), selectivity for a specific chemical reaction and reaction efficiency are high. Different.

  In addition, a metal material is widely used as the catalyst material, and a noble metal material is heavily used because of particularly good reactivity. For example, Patent Document 1 discloses a noble metal catalyst that is selective in a specific reaction. In recent years, an oxide catalyst has attracted attention, and Patent Document 2 discloses an oxide catalyst excellent in catalytic activity and selectivity.

JP 2007-090164 A JP 2007-301470 A

  However, in the reduction reaction of carbon dioxide, the chemical reaction with selectivity has not been sufficiently controlled, and the target product has not been obtained with high reaction efficiency. Therefore, development of a catalyst that can control the reduction reaction of carbon dioxide with high selectivity is desired.

  Accordingly, the present invention has been made in view of the above problems, and a metal-containing cluster catalyst capable of promoting and controlling the reduction reaction of carbon dioxide with high catalytic activity and selectivity, and carbon dioxide reduction using the same. It is an object to provide an electrode for use and a carbon dioxide reduction device.

  As a result of intensive studies to solve the above problems, the present inventors have found that a metal-containing cluster catalyst containing a specific metal exhibits excellent performance in the reduction reaction of carbon dioxide.

That is, the gist configuration of the present invention is as follows.
[1] A catalyst used for reducing carbon dioxide,
A metal in which the catalyst is a cluster comprising one metal atom (M) selected from gold, silver, copper, platinum, rhodium, palladium, nickel, cobalt, iron, manganese, chromium, iridium and ruthenium Containing cluster catalyst.
[2] The metal-containing cluster catalyst according to [1], wherein the cluster is made of a metal oxide containing the metal atom (M).
[3] The metal-containing cluster catalyst according to [1] or [2], wherein the cluster is composed of a single metal or a metal oxide represented by the following general formula (1).
M _n O _m (1)
However, in the said Formula (1), M represents the said metal atom (M), n and m are integers, n is 30 or less, m is a m / n ratio with respect to n, 0- 2.
[4] The metal-containing cluster catalyst according to [3], wherein in the formula (1), m is an integer such that m / n is 0.5 to 1.5 in relation to n.
[5] The metal-containing cluster catalyst according to any one of [1] to [4], wherein a primary particle size of the cluster is 0.1 to 3.0 nm.
[6] An electrode for carbon dioxide reduction comprising the metal-containing cluster catalyst according to any one of [1] to [5].
[7] A carbon dioxide reduction device comprising the carbon dioxide reduction electrode according to [6].

  The metal-containing cluster catalyst of the present invention exhibits excellent performance in the reduction reaction of carbon dioxide.

FIG. 1 is a block diagram showing the configuration of the electrolysis apparatus 1. FIG. 2A is a schematic diagram illustrating the configuration of the electrolytic cell 3, and FIG. 2B is a diagram illustrating the configuration of the electrolytic cell 3a. FIG. 3 is an overall schematic diagram showing an electrode generating device 27 used when producing an electrode having a copper porous body according to a comparative example of the present invention. FIG. 4 is a schematic diagram illustrating a reduction test apparatus 50 when a reduction test is performed in the embodiment. FIG. 5 is an enlarged schematic view showing the electrolytic cell 53 portion (H portion) of the reduction test apparatus 50 of FIG.

  Embodiments of a metal-containing cluster catalyst according to the present invention, a carbon dioxide reduction electrode and a carbon dioxide reduction device using the same will be described in detail below.

  The metal-containing cluster catalyst according to this embodiment includes gold (Au), silver (Ag), copper (Cu), platinum (Pt), rhodium (Rh), palladium (Pd), nickel (Ni), and cobalt (Co). And a cluster containing one metal atom (M) selected from iron (Fe), manganese (Mn), chromium (Cr), iridium (Ir) and ruthenium (Ru). Here, the “cluster” is an atomic group in which a plurality of atoms are bonded.

  Such a metal-containing cluster catalyst is suitably used as a catalyst for reducing carbon dioxide because it exhibits excellent performance in the reduction reaction of carbon dioxide.

  The metal atom (M) contained in the cluster according to this embodiment is one kind selected from Au, Ag, Cu, Pt, Rh, Pd, Ni, Co, Fe, Mn, Cr, Ir, and Ru. Such a cluster (hereinafter referred to as “metal-containing cluster”) exhibits excellent performance in the reduction reaction of carbon dioxide. Among them, the metal atom (M) is preferably one selected from Cu, Ag, Pd, and Au from the viewpoint of excellent reduction performance, and in particular, a hydrocarbon (methane) selectively in the reduction reaction of carbon dioxide. Cu is more preferable in that it can be produced.

  Further, the metal-containing cluster is not particularly limited as long as it contains the metal atom (M) as described above, and includes a simple substance of the metal atom (M), an alloy containing the metal atom (M), and a metal atom (M). It may be a cluster composed of any of a metal oxide containing or a composite oxide containing a metal atom (M). The alloy or composite oxide containing a metal atom (M) is at least one metal selected from Au, Ag, Cu, Pt, Rh, Pd, Ni, Co, Fe, Mn, Cr, Ir, and Ru. Any alloy or composite oxide containing an atom may be used, and an alloy or composite oxide containing two or more metal atoms selected from the above, or any other metal atom that can be alloyed or compounded with the metal atom (M) It may be an alloy or composite oxide containing. Moreover, it is preferable that a metal containing cluster consists of a metal oxide containing a metal atom (M) especially.

Moreover, it is preferable that a metal containing cluster consists of a metal oxide containing the simple substance of a metal atom (M) or a metal atom (M) represented by following General formula (1).
M _n O _m (1)
In the above formula (1), M represents the above metal atom (M), and O represents an oxygen atom.
N and m are integers.

  Further, in the above formula (1), n is preferably 30 or less, more preferably 15 or less. Further, n is preferably 6 or more, more preferably 9 or more. By setting it as the said range, control of an oxidation degree (valence) can be performed with control of a cluster size.

  In the above formula (1), m is preferably 0 to 2, and more preferably 0.5 to 1.5, and even more preferably 0.55, in relation to n. ~ 0.75. By setting it as the said range, catalyst performance increases because it becomes the oxidation degree peculiar to a cluster. In the above formula (1), when m / n is 0, the metal-containing cluster is composed of a single metal atom (M).

  Moreover, it is preferable that the primary particle size of a metal containing cluster is 0.1-3.0 nm, More preferably, it is 0.5-2.0 nm, More preferably, it is 0.6-1.2 nm. By setting it as the said range, a catalyst performance increases by obtaining the oxidation degree peculiar to a cluster with the increase in the surface area of the whole particle | grains of a metal containing cluster. The primary particle size is measured by mass spectrometry (MS), transmission electron microscope (TEM), dynamic light scattering method (DLS), or the like.

  Such metal-containing clusters can be produced in a liquid phase or a gas phase by a known method. Examples of the method for producing in the liquid phase include a method using a dendrimer. Examples of the method for producing in the gas phase include an ion sputtering method, a plasma discharge method, and a laser evaporation method (laser ablation). Especially, it is preferable to manufacture by the method using laser ablation or a dendrimer from a viewpoint of manufacturing efficiently a metal containing cluster containing the metal atom (M) which has a special valence.

  Here, laser ablation is a phenomenon in which clusters are scattered by irradiating a solid laser surface with a strong laser beam and locally evaporating a surface layer that has become hot. In addition, it may be called laser sputtering. In addition, the apparatus which performs laser ablation is not specifically limited, It can carry out using a well-known apparatus.

  Moreover, the method using a dendrimer is not specifically limited, It can carry out by using a well-known method. For example, a solution containing a dendrimer and a solution of a metal compound corresponding to the target metal-containing cluster are mixed to synthesize a metal complex of a dendrimer. (1) Reduction using a reducing agent such as sodium borohydride, A method of reducing the metal complex by electrochemical reduction, photochemical reduction, etc. and precipitating the metal on the dendrimer, or (2) removing the solvent by heating the solution containing the dendrimer metal complex, A metal cluster can be generated by a method of depositing a metal or a salt thereof. Examples of the dendrimer include polyamidoamine (PAMAM) dendrimer, polypropyleneimine (PPI) dendrimer, phenylazomethine dendrimer (DPA), and the like. Examples of the metal compound include metal chlorides and nitrates corresponding to the target metal-containing cluster. Moreover, well-known solvents, such as water and alcohol, can be used for a solvent, for example.

  Furthermore, by firing the metal-containing cluster obtained as described above, a carbon material containing the metal-containing cluster is obtained. When such baking is performed at a high temperature (for example, 400 ° C. or higher), it is performed in an inert gas atmosphere such as nitrogen or a rare gas such as argon, and at a relatively low temperature (for example, 200 ° C. or higher). If done, it can be done in air. Further, after the baking as described above, a heat treatment can be further performed in a reducing atmosphere such as hydrogen.

  Further, the usage form of the metal-containing cluster catalyst according to the present embodiment is not particularly limited, but it is preferably supported on a carrier and used as a composite material.

  The carrier is not particularly limited, and examples thereof include carbon, metal, semiconductor, ceramic, and polymer. The carrier may be appropriately selected according to the use of the composite material or the usage environment. Specifically, when the composite material is used as a conductive material, it is preferable to use carbon or metal as the carrier. When is used as a photocatalyst, it is preferable to use a semiconductor as a carrier.

  As the polymer used as the carrier, for example, a chain polymer or a single polymer can be suitably used. Examples of the chain polymer include polyvinyl pyrrolidone (PVP), polyethylene glycol (PEG), and polyvinylidene fluoride (PVdF). Examples of the single polymer include ferritin, thiolate, phosphine, and alkyne. It is done.

  Further, the metal-containing cluster catalyst according to the present embodiment can be suitably used as a material for an electrode for carbon dioxide reduction. Therefore, the carbon dioxide reduction electrode according to the present embodiment preferably includes the metal-containing cluster catalyst as described above. The formation method of an electrode is not specifically limited, It can carry out by a well-known method.

  Specifically, for example, the carbon material of the metal-containing cluster containing the above-mentioned dendrimer is dispersed in a solvent, mixed with a binder, and further mixed with a conductive material as necessary to form a paint. An electrode containing a metal-containing cluster catalyst can be produced by directly applying to a current collector, an ion exchange membrane or the like and drying.

  The binder is not particularly limited, and examples thereof include polyvinylidene fluoride (PVdF), a mixture of sodium carboxymethyl cellulose (CMC) and styrene butadiene copolymer (SBR), and polytetrafluoroethylene (PTFE).

  Such an electrode including the metal-containing cluster catalyst according to the present invention can be suitably used as a cathode electrode of a carbon dioxide reduction device described later.

  The carbon dioxide reduction device according to the present embodiment preferably includes the carbon dioxide reduction electrode as described above. The method for forming the device is not particularly limited, and can be performed by a known method.

  Hereinafter, the electrolysis apparatus 1 shown in FIG. 1 will be described as an example of the carbon dioxide reduction apparatus according to the present embodiment. In FIG. 1, the electrolyzer 1 is mainly composed of an electrolysis cell 3, a gas recovery device 5, an electrolyte solution circulation device 7, a carbon dioxide supply unit 9, a power source 11, and the like. In addition, it cannot be overemphasized that the carbon dioxide reducing apparatus which concerns on this embodiment is not limited to the structure of FIG. 1, It can change suitably as needed and can be used.

  The electrolysis cell 3 is a part that reduces the target substance. In the present embodiment, particularly, carbon dioxide (including a case where the solution is carbonate ion or carbonate. Hereinafter, simply referred to as carbon dioxide or the like) is reduced. It is a part to do. Electric power is supplied to the electrolysis cell 3 from the power supply 11. The details of the electrolytic cell 3 will be described later.

  The electrolytic solution circulation device 7 is a part that circulates the cathode side electrolytic solution with respect to the cathode electrode of the electrolytic cell 3.

  The carbon dioxide supply unit 9 is, for example, a tank that stores carbon dioxide, and can hold carbon dioxide and supply a predetermined amount of carbon dioxide to the electrolyte circulation device 7. Instead of carbon dioxide, a solution already in the form of carbonate ions, carbonates, or the like can be held and a predetermined amount can be supplied to the electrolyte circulation device 7.

  The gas recovery device 5 is a part that recovers the gas generated by reduction by the electrolytic cell 3. In the gas recovery device 5, it is possible to collect gas such as hydrocarbons generated at the cathode electrode of the electrolysis cell 3. In the gas recovery device 5, the gas may be separable for each gas type.

  The electrolyzer functions as follows. As described above, an electrolytic potential from a power source is applied to the electrolytic cell. The electrolytic solution is supplied to the cathode electrode of the electrolytic cell by the electrolytic solution circulation device. At the cathode electrode of the electrolytic cell, carbon dioxide or the like in the supplied electrolyte is reduced. When carbon dioxide and the like are reduced, hydrocarbons such as ethane and ethylene are mainly produced.

  The hydrocarbon gas generated at the cathode electrode is recovered by a gas recovery device. In the gas recovery apparatus, it is possible to separate and store the gas as necessary.

  By reducing and consuming carbon dioxide and the like at the cathode electrode, the concentration of carbon dioxide and the like in the electrolyte decreases. Carbon dioxide or the like that has been reduced by the reduction reaction is always replenished, and its concentration is always kept within a predetermined range. Specifically, a part of the electrolytic solution is recovered by an electrolytic solution circulation device, and an electrolytic solution having a predetermined concentration is always supplied. As described above, in the electrolytic cell 3, hydrocarbons can always be generated under a certain condition.

  Next, details of the electrolytic cell 3 will be described. FIG. 2A is a diagram illustrating an example of the configuration of the electrolytic cell 3. The electrolytic cell 3 mainly includes a tank 16a that is a cathode tank, a metal mesh 17, a cathode electrode 19, an ion exchange membrane 21, an electrolyte 23, an anode electrode 25, a tank 16b that is an anode tank, and the like. In addition, it cannot be overemphasized that the electric cell of the carbon dioxide reduction apparatus which concerns on this embodiment is not limited to the structure of Fig.2 (a), A structure can be changed suitably and used as needed.

  Electrolytes 15a and 15b are held in the cathode tank 16a and the anode tank 16b, respectively. In the upper part of the tank 16a on the cathode electrode side, a hole for recovering the generated gas is formed and connected to a gas recovery device (not shown). That is, the gas generated at the cathode electrode is recovered from the hole. Moreover, piping etc. are connected to the cathode tank 16a, and it connects with the electrolyte solution circulation apparatus 7 which abbreviate | omitted illustration. That is, the electrolytic solution 15a in the cathode tank 16a can always be circulated by the electrolytic solution circulation device 7. If necessary, the electrolytic solution on the anode tank 15b side may be circulated similarly.

  The electrolytic solution 15a that is a cathode electrolytic solution is preferably an electrolytic solution that can dissolve a large amount of carbon dioxide or the like. For example, an alkaline solution such as a sodium hydroxide aqueous solution or a potassium hydroxide aqueous solution, monomethanolamine, methylamine, In addition, a liquid amine or a mixture of the liquid amine and an aqueous electrolyte solution is used. Also. Acetonitrile, benzonitrile, methylene chloride, tetrahydrofuran, propylene carbonate, dimethylformamide, dimethyl sulfoxide, methanol, ethanol and the like can be used.

  Here, the aqueous electrolyte solution is not particularly limited, and for example, an aqueous potassium chloride solution, an aqueous sodium chloride solution, an aqueous sodium hydroxide solution, an aqueous potassium hydroxide solution, an aqueous sodium hydrogen carbonate solution, an aqueous potassium carbonate solution, or the like can be used.

  Moreover, there is no restriction | limiting in particular as the electrolyte solution 15b which is an anode electrolyte solution, For example, potassium chloride aqueous solution, sodium chloride aqueous solution, sodium hydrogencarbonate aqueous solution, potassium hydrogencarbonate aqueous solution etc. can be used.

  The metal mesh 17 is a member that is connected to the negative electrode side of the power source and energizes the cathode electrode 19. The metal mesh 17 is, for example, a copper mesh or a stainless steel mesh. For example, stainless steel SUS304 400 mesh (thickness 25 μm, manufactured by Nilaco Corporation) can be used.

  Although there is no restriction | limiting in particular as the ion exchange membrane 21, For example, a hydrocarbon type | system | group, a perfluorocarbon type | system | group, etc. can be used. An anion exchange membrane is particularly desirable, and a Nafion membrane, a polyvinylidene fluoride (PVDF) membrane, or the like can be used. For example, “Selemion (registered trademark) AMV” manufactured by Asahi Glass Co., Ltd. can be used. The ion exchange membrane 21 is used when manufacturing the cathode electrode 19 described later, and functions as a support member for the metal-containing cluster catalyst that constitutes the cathode electrode 19. In addition, if an ion exchange membrane is used as the supporting member, the configuration of the reducing portion during electrolysis described later becomes easy.

  The electrolyte 23 is provided as necessary. The electrolyte 23 interposed between the ion exchange membrane 21 and an anode electrode 25 described later is not particularly limited, but is a polymer electrolyte such as polyvinylidene fluoride, polyacrylic acid, polyethylene oxide, polyacrylonitrile, polymethyl methacrylate. Alternatively, an aqueous potassium chloride solution, an aqueous sodium chloride solution, or the like can be used.

  The anode electrode 25 is connected to the positive electrode of the power source. Although there is no restriction | limiting in particular as the anode electrode 25, For example, titanium, platinum, titanium (Ti / Pt) which carried out platinum coating, stainless steel, copper, carbon, etc. can be used. In particular, Ti / Pt is preferable from the viewpoint of little deterioration. The shape is not particularly limited and can be a plate shape, punched metal, mesh shape, or non-woven shape, but the viewpoint of reducing the thickness of the electrolysis cell and the shape of the electrolysis cell may be curved. From the viewpoint that it can be used, a nonwoven fabric is preferable.

  As the cathode electrode 19, an electrode including the metal-containing cluster catalyst according to the present invention is used. By using the electrode containing the metal-containing cluster catalyst according to the present invention as the cathode electrode 19, the reduction amount of carbon dioxide can be increased, the reduction reaction of carbon dioxide can be selectively controlled, and the reduction efficiency in terms of selectivity. Can be improved.

  Here, as the electrolysis cell according to the present embodiment, an electrolysis cell 3a as shown in FIG. 2B can also be used. The electrolysis cell 3a has substantially the same configuration as the electrolysis cell 3, but the elements are sequentially arranged from the center to the outer periphery in the radial direction on a substantially concentric circle with respect to the electrolysis cell 3 in which the plate-like elements are stacked. The In addition, since each element which comprises the electrolytic cell 3a is the same as the element which comprises the electrolytic cell 3, the overlapping description is abbreviate | omitted.

  As mentioned above, although embodiment of this invention was described, this invention is not limited to the said embodiment, All the aspects included in the concept of this invention and a claim are included, and various within the scope of this invention. Can be modified.

  Next, in order to further clarify the effects of the present invention, examples and comparative examples will be described, but the present invention is not limited to these examples.

Example 1
First, a phenyl azomethine dendrimer copper complex was synthesized by mixing a chloroform solution of phenyl azomethine dendrimer and an acetone solution of 12 molar equivalents of copper chloride with respect to the dendrimer. Next, an excess amount of sodium borohydride was added to this solution to reduce the phenylazomethine dendrimer copper complex, thereby synthesizing a phenylazomethine dendrimer copper cluster. Moreover, the carbon material which included the copper containing cluster was synthesize | combined by baking the synthesized phenyl azomethine dendrimer copper cluster in nitrogen atmosphere.

  Further, the obtained carbon material containing the copper-containing cluster was dispersed in N-methyl-2-pyrrolidone (NMP), and polyvinylidene fluoride (PVDF) was added as a binder to this dispersion. The mixture was made into a paint, applied onto an ion exchange membrane and dried to produce an electrode containing a copper-containing cluster catalyst.

(Example 2)
In Example 2, the firing atmosphere of the phenylazomethine dendrimer copper cluster was changed to the air atmosphere instead of the nitrogen atmosphere, and the copper-containing cluster was formed in the same manner as in Example 1 except that the firing temperature was lower than that in Example 1. An electrode including an encapsulated carbon material and a copper-containing cluster catalyst using the carbon material was produced.

(Example 3)
Example 3 is a carbon material containing a copper-containing cluster in the same manner as in Example 1 except that the firing temperature of the phenylazomethine dendrimer copper cluster is lower than that of Example 1, and a copper-containing material using this carbon material. An electrode containing a cluster catalyst was prepared.

Example 4
Example 4 uses a carbon material containing a copper-containing cluster in the same manner as in Example 1 except that a phenylazomethine dendrimer copper cluster is further fired in a hydrogen atmosphere after firing in a nitrogen atmosphere, and a carbon material containing the copper-containing cluster is used. An electrode containing a copper-containing cluster catalyst was prepared.

(Example 5)
Example 5 is the same method as Example 1 except that a phenylazomethine dendrimer silver complex was synthesized by mixing a chloroform solution of phenylazomethine dendrimer with an acetone solution of 12 molar equivalents of silver nitrate with respect to the dendrimer. Thus, an electrode including a carbon material containing silver-containing clusters and a silver-containing cluster catalyst using the carbon material was produced.

(Comparative Example 1)
In Comparative Example 1, copper was deposited on the ion exchange membrane by an electroless plating method by the method shown below, and an electrode having a copper porous body in which the deposited copper particles were collected was obtained.
First, 30 mL of a 5 mmol / L aqueous copper acetate solution is placed in the tank 29a of the electrode manufacturing apparatus 27 shown in FIG. 3, and a 12% by mass sodium borohydride solution (14 mol / L NaOH, manufactured by Aldrich) is stored in the tank 29b. A mixed solution of 142 μL and 29.858 mL of distilled water was added. The electrode manufacturing apparatus 27 having such a configuration was allowed to stand at room temperature for 1 hour, and copper was deposited on the ion exchange membrane 21 by an electroless plating method to obtain an electrode having a copper porous body.

(Comparative Example 2)
The comparative example 2 obtained the electrode which has a copper porous body by the method similar to the comparative example 1 except having baked the electrode produced by the comparative example 1 in air | atmosphere atmosphere.

(Comparative Example 3)
The comparative example 3 obtained the electrode which has a copper porous body by the method similar to the comparative example 1 except having baked the electrode produced by the comparative example 1 in nitrogen atmosphere.

(Comparative Example 4)
Comparative Example 4 was the same as Comparative Example 1 except that 30 mL of the 5 mmol / L aqueous copper acetate solution of Comparative Example 1 was changed to 30 mL of a 5 mmol / L aqueous silver nitrate solution to produce an electrode having a silver porous body. went.

[Evaluation]
For the catalysts according to the above Examples and Comparative Examples, the following characteristic evaluation was performed. The evaluation conditions for each characteristic are as follows. The results are shown in Table 1.

[1] Composition and valence of metal (M) About the metal-containing cluster and metal-containing porous body constituting the catalyst, composition analysis and valence evaluation are performed using inductively coupled plasma sample analysis and X-ray photoelectron spectroscopy. went.
Moreover, the samples for an analysis used Examples 1-5 as the carbon material containing the copper containing cluster before electrode preparation, and Comparative Examples 1-4 used the metal material which scraped off and separated the porous body part on an ion exchange membrane.

[2] Primary particle size Examples 1 to 5 are transmission types for carbon materials containing metal-containing clusters before electrode preparation, and Comparative Examples 1 to 4 are transmission types for metal-containing porous bodies collected from the ion exchange membrane. Using an electron microscope (TEM, manufactured by JEOL Ltd.), each particle was photographed at a magnification at which the contours of primary particles (single particles not agglomerated with other particles) can be clearly recognized. The following analysis was performed for each example and comparative example. First, 100 particles (primary particles) were randomly selected from the photographed image, the projected area for each particle was obtained by an image processing apparatus, and the total occupied area of the particles was calculated from the total of them. Divide this total occupied area by the number of selected particles (100) to calculate the average occupied area per particle, and calculate the diameter of the circle corresponding to this area (average equivalent circle diameter per particle). The primary particle size was used.

[3] Reduction Test; Gas Concentration and Current Efficiency The reduction test was performed using a carbon dioxide reduction test apparatus 50 shown in FIG. Here, the electrodes according to Examples and Comparative Examples were used as the cathode electrode 69a. FIG. 5 is a diagram showing the electrolysis cell 53, and is an enlarged view of a portion H in FIG. The reduction test apparatus 50 mainly includes a first tank 51a, a second tank 51b, an electrolytic cell 53, a power source 55, an analysis tube 59, a supply tube 61, and the like.

  The two tanks 51 a and 51 b are partitioned by the electrolytic cell 53. Sodium hydrogen carbonate 57 is placed in each of the first tank 51a and the second tank 51b. As the sodium hydrogen carbonate solution 57, a 50 mmol / L sodium hydrogen carbonate solution was used, and 30 mL of solution was used in each tank. On the first tank 51a side, the upper part is sealed with a lid, and a supply pipe 61 and an analysis pipe 59 are provided so as to penetrate the lid. The supply pipe 61 is connected to a carbon dioxide supply source (not shown), and the end thereof is immersed in the sodium hydrogen carbonate solution 57. The end portion of the supply pipe 61 extends to the vicinity of the lower bottom portion of the first tank 51a. The sodium hydrogen carbonate solution 57 in the first tank 51a is constantly stirred by the supply of carbon dioxide from the supply pipe 61, and the concentration thereof is kept substantially constant. Therefore, the same effect as circulating the sodium hydrogen carbonate solution 57 in the first tank 51a can be obtained.

  The end of the analysis tube 59 passes through the lid, and is disposed in the gas portion between the lid and the solution water surface without contacting the sodium hydrogen carbonate solution 57. That is, the analysis tube 59 can collect the generated gas and the like. The analysis tube 59 is connected to a gas analyzer (not shown), and the collected gas is led to the analyzer.

  As shown in FIG. 5, the electrolytic cell 53 includes a copper-containing cluster catalyst 63 that is a cathode electrode on an ion exchange membrane 65 (this is the case of the electrode of the example. In the case of the electrode of the comparative example, the copper porous The metal mesh 73 is formed so as to sandwich the copper-containing cluster catalyst 63 therebetween. That is, the metal mesh, the copper-containing cluster catalyst, and the ion exchange membrane are arranged in this order from the first tank 51a side, and are sandwiched between the cathode electrode 69a and the anode electrode 69b. Further, it is sandwiched between the cathode electrode 69a and the anode electrode 69b from the outside with the seal member 71, and fixed with a clamp or the like (not shown).

  Here, a rubber packing was used as the seal member 71. The cathode electrode 69a is a member for energizing the metal mesh 73, and a ring-shaped Ti / Pt electrode was used. The metal mesh 73 is a copper mesh and is in electrical contact with the copper-containing cluster catalyst 63 and also functions as a cathode. The copper mesh used was “copper 100 mesh wire mesh” (thickness 0.11 mm, manufactured by Nilaco Corporation). The copper-containing cluster catalyst 63 is an electrode produced in the above example (or comparative example). As the ion exchange membrane 65, “Celemion (registered trademark) AMV” manufactured by Asahi Glass Co., Ltd. was used.

  As the anode electrode 69 b, a ring-shaped Ti / Pt electrode that holds the metallic nonwoven fabric 67 that is an anode electrode and is in electrical contact with the metallic nonwoven fabric 67 is used. The metal nonwoven fabric 67 was a Pt nonwoven fabric. That is, the metal nonwoven fabric 67 is held in the ring of the ring-shaped anode electrode 69b.

  As shown in FIG. 4, the cathode electrode 69 a and the anode electrode 69 b are connected to a power supply 55. In the reduction test, electrolysis was performed for 60 minutes at a current value of 2 mA and a voltage of 2.8 V using the cathode electrode 69a as a cathode and the anode electrode 69b side as an anode.

  At this time, carbon dioxide gas was bubbled from the supply pipe 61 at a rate of 10 mL / min into the tank 69a on the metal mesh 73 and copper-containing cluster catalyst 63 side (the opposite side to the ion exchange membrane 65) (in the direction of arrow F in the figure). ). The gas generated from the cathode was collected by the analysis tube 59 (in the direction of arrow G in the figure) and analyzed by gas chromatography. SUPELCO CARBOXEN 1010PLOT 30m × 032mmlD was used as a column, and FID was used as a detector.

As the reaction at the cathode electrode, we focused on the generation of methane, ethylene and ethane as shown below.
CO ₂ + 8H ⁺ + 8e ⁻ → CH ₄ + 2H ₂ O
CO ₂ + 12H ⁺ + 12e ⁻ → C ₂ H ₄ + 4H ₂ O
CO ₂ + 14H ⁺ + 14e ⁻ → C ₂ H ₆ + 4H ₂ O

The reaction at the anode electrode is as follows.
2H ₂ O → 4H ⁺ + 4e ⁻ + O ₂

  Furthermore, current efficiency (Faraday efficiency) was calculated based on the gas amount of the obtained product and the input current.

  As shown in Table 1, it was confirmed that the metal-containing cluster catalysts (Examples 1 to 5) were excellent in catalytic activity as compared with the porous catalyst (Comparative Examples 1 to 4).

  Specifically, the copper-containing cluster catalyst according to Examples 1 to 4 has a larger amount of product due to the reduction of carbon dioxide than the catalyst of the porous body according to Comparative Examples 1 to 3 that also uses copper. It was confirmed that the activity was excellent.

  Further, the silver-containing cluster catalyst according to Example 5 has a large amount of product due to reduction of carbon dioxide and is excellent in catalytic activity as compared with the porous catalyst according to Comparative Example 4 which also uses silver. confirmed.

  Further, the copper-containing cluster catalyst (Examples 1 to 4) has a larger amount of hydrocarbons (methane, ethylene, ethane) produced by the reduction reaction of carbon dioxide than the silver-containing cluster catalyst (Example 5). It was confirmed that the hydrogen selectivity was excellent.

(Examples 6 to 27)
In Examples 6 to 27, the number of generations of phenylazomethine dendrimers, equivalents of raw materials, and firing conditions of phenylazomethine dendrimer copper clusters were appropriately changed, and copper-containing clusters were encapsulated in the same manner as in Example 1. An electrode including a carbon material and a copper-containing cluster catalyst using the carbon material was produced, and the same evaluation as in Example 1 was performed. The results are shown in Table 2. In Table 2, Examples 1 to 4 are the same as those shown in Table 1.

As shown in Table 2, the copper-containing clusters represented by Cu _n O _m is the ratio of m / n is, when it is 0.67, it was confirmed that exhibits particularly excellent catalytic activity (performed Examples 1, 6, 9, 15 and 27). Among such copper-containing clusters represented by Cu _n O _m having an m / n ratio of 0.67, particularly when n is 12 (Example 1), all products can be produced most. It was confirmed that the catalyst efficiency was particularly excellent.

DESCRIPTION OF SYMBOLS 1 ......... Electrolyzer 3, 3a ......... Electrolytic cell 5 ......... Gas recovery device 7 ......... Electrolyte circulation device 9 ......... Carbon dioxide supply part 11 ......... Power supply 13 ......... Separators 15a, 15b ……… Electrolytes 16a, 16b ……… Bath 17 ………… Metal mesh 19 ………… Cathode electrode 21 ………… Ion exchange membrane 23 ……… Electrolyte 25 ……… Anode electrode 27 ……… Electrode generator 29a , 29b ......... tank 31 ......... sealing member 33 .... reducing agent aqueous solution 35 .... copper ion aqueous solution 50 .... reduction test apparatus 51a, 51b .... tank 53 .... electrolysis cell 55 .... Power source 57... Sodium bicarbonate solution 59... Analysis tube 61... Supply tube 63... Copper-containing cluster catalyst or copper porous body 65. 69b ......... Electrode 71 ......... Sh Seal member 73 ......... metal mesh

Claims (7)

A catalyst used to reduce carbon dioxide,
A metal in which the catalyst is a cluster comprising one metal atom (M) selected from gold, silver, copper, platinum, rhodium, palladium, nickel, cobalt, iron, manganese, chromium, iridium and ruthenium Containing cluster catalyst.   The metal-containing cluster catalyst according to claim 1, wherein the cluster is made of a metal oxide containing the metal atom (M). The metal-containing cluster catalyst according to claim 1 or 2, wherein the cluster is composed of a single metal or a metal oxide represented by the following general formula (1).
M _n O _m (1)
However, in the said Formula (1), M represents the said metal atom (M), n and m are integers, n is 30 or less, m is a m / n ratio with respect to n, 0- 2.   4. The metal-containing cluster catalyst according to claim 3, wherein in the formula (1), m is an integer such that m / n is 0.5 to 1.5 in relation to n.   The metal-containing cluster catalyst according to any one of claims 1 to 4, wherein a primary particle size of the cluster is 0.1 to 3.0 nm.   The electrode for carbon dioxide reduction containing the metal containing cluster catalyst of any one of Claims 1-5.   A carbon dioxide reduction device comprising the carbon dioxide reduction electrode according to claim 6.

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